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Process Equipment and Plant Design

Process Equipment and Plant Design
With increase in the number of shell passes, the value of FT

Remains same
Increases
Remains same, only if the number of tube passes does not change
Decreases

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Process Equipment and Plant Design
Length to diameter ratio of most rotary driers is in the range of

20 to 30
1 to 2
4 to 10
10 to 20

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Process Equipment and Plant Design
The ratio of volumes of the mixed reactor to the plug flow reactor (for identical feed composition, flow rate, conversion, and for all positive reaction orders) is always

1
Equal to the order of reaction
>1
< 1

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Process Equipment and Plant Design
Bubble cap diameter used for the distillation column having diameter ranging from 1.5 to 4.5 metres is about __________ mm.

10
50
150
100

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Process Equipment and Plant Design
Minimum tube pitch recommended for shell and tube heat exchangers is about __________ times the outside diameter of the tube.

2.5
1.75
3.5
1.25

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Process Equipment and Plant Design
Steam is preferred to be used as a heating medium in heat exchangers, because of its

Low cost
Non-corrosive condensate
High film co-efficient
High latent heat

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